Apparatus for aboveground separation, vaporization and recovery of oil from oil shale

ABSTRACT

A retort apparatus for recovering oil from crushed oil shale moved through an elongated housing, includes a plurality of heat exchangers located in the housing for transferring heat to or from the shale. The heat exchangers are spaced to define in sequence a drying zone, a preheating zone, a cracking and distillation zone, and a waste heat recovery zone. An auxiliary heating assembly connected to the heat exchangers delivers sufficient heat to raise the temperature of the shale in the cracking and distillation zone to the critical temperature for separating hydrocarbons in vapor form therefrom. The tubes of the heat exchangers are elongated ovals in cross-section and are offset from each other in alternate rows to increase the area of heat exchange and to reduce the temperature drop between the entering heated air and exiting heated air flowing through each heat exchange tube. The heat exchange tubes include common fins which encase banks of the tubes, with the fins on the banks of tubes being aligned with each other to provide passage for flow of crushed oil shale therethrough. A separating device is connected to the cracking and distillation zone to withdraw hydrocarbon vapors released from the shale and to condense the hydrocarbons. Additionally, the retort apparatus includes a device associated with the separating device for maintaining a predetermined operating pressure in the preheat and waste heat recovery zones to prevent separated hydrocarbon vapors from leaking to the atmosphere.

REFERENCE TO RELATED APPLICATION

This application is a Continuation-In-Part of U.S. patent application Ser. No. 457,975, filed Jan. 14, 1983 now U.S. Pat. No. 4,502,920 entitled Apparatus for Aboveground Separation, Vaporization and Recovery of Oil from Oil Shale.

BACKGROUND OF THE INVENTION

This invention relates generally to a retorting type apparatus, process and system for aboveground recovery of oil from oil shale and more particularly to an anaerobic retorting apparatus, process and system for separating, vaporizing and recovering oil and gas from crushed oil shale.

Many aboveground retorting processes are known in the prior art. Only a few of these retorting apparatus, processes and systems however have been constructed and studied for the purpose of developing an apparatus and system suitable for handling the recovery of oil from the large quantities of oil shale material that must be handled to meet the modern requirements for an efficient workable, and feasible system.

Those skilled in the art will recognize that a technically and economically feasible retorting apparatus, process and system must be capable of thermally degrading the solid organic material (kerogen) in the shale. Thus, such retorting apparatus, processes and systems must be capable of heating the oil shale to 800°-1100° F. (425°-600° C.), to decompose the kerogen into the oil and gaseous components so that these components can be separated and recovered from the base material of the shale.

Various types of apparatus and systems for aboveground retorting processes for removing oil and gas from oil shale have been designed, developed and tested in the United States. These are generally identified as the Gas Retorting System, and the Tosco II Retorting System. The apparatus and system for these prior art processes and the respective pros and cons thereof are outlined in depth at Chapter 9 entitled Retorting Technology of Oil Shale by Gerald U. Dinneen in the publication, Developments in Petroleum Science, 5; Oil Shale edited by T. F. Yen and G. V. Chilingarian published in 1976 by American Elsevier Scientific Publishing Company, New York, N.Y. 10017.

In Brazil, Petrobras, a Brazilian Government Corporation has developed an aboveground retorting process identified as the Petrosix process. In this Petrosix process a vertical retort tower is charged with ground oil shale which is moved by gravity from the top to the bottom thereof through heating, retorting, and cooling zones, in which a recycled gas stream entering at the bottom of the vertical retort tower recovers heat as it moves upwardly in a counter-flow direction to the downwardly moving oil shale until it reaches an intermediate or medial section of the vertical retort tower where it combines with heated retort gas for providing the necessary heat to raise the temperature of the downwardly moving oil shale to the required decomposition temperatures for separating and vaporizing oil and gas from the oil shale. The entire mixture of recycled and heated gases, separated and vaporized oil, all move upwardly in counter-flow to the entering oil shale and pass from a suitable outlet or discharge port at the upper end of the vertical retort tower. The mixture is then passed to means for separating the product oil and product gas. A portion of the product gas is recycled for reuse in the vertical retort tower. This process is characterized by the use of an external heat source and by direct heat exchange between the solid oil shale and the upflowing gaseous heat exchange medium which is used to establish the temperature required for decomposition of the organic matter in the downwardly moving oil shale in the vertical retort tower. The following U.S. patents were cited in related U.S. patent application Ser. No. 508,738, filed June 29, 1983, which, in turn, is a divisional application of the aforementioned U.S. patent application Ser. No. 457,975: U.S. Pat. No. 2,448,223 to Lantz; U.S. Pat. No. 2,581,041 to Ogorzaly et al; U.S. Pat. No. 2,698,283 to Dalin, U.S. Pat. No. 2,710,828 to Scott, Jr.; U.S. Pat. No. 3,384,569 to Peet; U.S. Pat. No. 3,377,266 to Salnikov; and U.S. Pat. No. 4,056,461 to Unverferth. The relevance of these references is discussed in the aforementioned U.S. patent application Ser. No. 508,738.

A problem that may result in prior art system due to improper pressure differentials is that the vaporized kerogen and components thereof may condense in the tower before being drawn off. This, of course, causes problems in the flow of material through the tower and may even be dangerous.

The present invention provides an improved retorting process in which an elongated tower defines a passage means for passing by gravitational movement crushed oil shale fragments generally in a size range not in excess of 3/4", through drying, preheating, cracking and distillation, and waste heat recovery zones formed in the elongated tower. These zones are established and characterized by indirect heat exchange means. The waste heat from the waste heat recovery zone is recovered and passed to both the cracking and distillation zone and preheat recovery zone. A separate externally heated gas stream or heat transfer fluid provides the heat exchange medium for the heating of the oil shale during its gravitational movement through the cracking and distillation zone. In the cracking and distillation zone, the preheated oil shale is raised to the required temperature for the decomposition of the kerogen organic matter. In the decomposed state the kerogen is vaporized and the hydrocarbon and gaseous components of the kerogen are, in the vapor state, readily separated from the gravitational moving crushed oil shale in the elongated housing or recovery tower. This separation process is controlled by maintaining atmospheric pressure in the elongated housing or recovery tower at two locations. Location No. 1 may be in the drying zone or the preheat zone. This will permit water vapor to exit from the top of the elongated housing or recovery tower. Location No. 2 is a predetermined distance from the discharge outlet for spent oil shale. By maintaining the pressure conditions in the elongated housing or recovery tower at atmospheric pressure, the decomposed kerogen vapors can be drawn off or will exit under pressure automatically from the cracking or distillation zone.

By this means the cracking and distillation zone will be at a pressure above atmospheric pressure and will operate in an ambient atmosphere substantially lacking in oxygen.

SUMMARY OF THE INVENTION

Thus the present invention covers an improved retort apparatus for recovering hydrocarbons from crushed oil shale having, an elongated housing with an inlet for crushed shale at one end, an outlet for spent crushed shale at the end of the housing remote from the inlet end, and a passage end to end therethrough enables the crushed oil shale to move from the inlet to the outlet. A plurality of heat exchange means connected in the housing for heat exchange relation with the crushed oil shale moving through the passage means are disposed serially between the inlet and the outlet to define, a drying zone, a preheating zone, a cracking and distillation zone, and a waste heat recovery zone. Circulating means is provided for passing waste heat recovered from the waste heat recovery zone to the preheating zone, and an auxiliary heating means connected to one of the plurality of heat exchanger means disposed in the cracking and distillation zone delivers heat sufficient to raise the temperature of the crushed oil shale moving through the passage means to the critical temperature for separating hydrocarbons in vapor form from the crushed oil shale. Separating means including a condenser operatively connected with the cracking and distillation zone acts to withdraw a mixture of hydrocarbon and gas vapors released from the heated crushed oil shale moving through the cracking and distillation zone, and to separate and recover the hydrocarbon therefrom, means connected for operative association with the outlet for the elongated housing controls the rate of movement of crushed oil shale through the passage means, and conveying means adjacent the outlet end of the elongated housing removes the spent oil shale discharged therefrom.

Additionally the retort apparatus as above described includes means for maintaining a predetermined operating pressure in the respective preheat zone and the waste heat recovery zone to prevent separated hydrocarbon and gas vapors from leaking to the atmosphere through either the inlet or the outlet for the elongated tower.

Further, the retort apparatus as described above includes means for sensing the pressures in the zones surrounding the cracking and distillation zone, and means for adjusting the pressure in the cracking and distillation zone in response to the sensed pressures and greater than the pressures in the other zones.

Additionally the retort apparatus as described above, includes means for venting hot gases from the auxiliary heating means for heating the cracking and distillation zone, and means connecting the one of the plurality of heat exchange means in the drying section to the means for venting the waste hot gases from the auxiliary heating means for drying the crushed oil shale entering the passage means in the elongated housing.

Accordingly it is an object of the present invention to provide an improved retort apparatus for separating hydrocarbon from oil shale.

Another object of the present invention is to provide an improved retort apparatus for separating hydrocarbons from oil shale in which the system is, boot-strapped, by recovering waste heat from spent oil shale and using waste heat from the cracking and distillation zone of the apparatus to preheat oil shale entering the system for retort treatment.

Another object of the present invention is to provide an improved retort apparatus for separating hydrocarbons from oil shale which includes, a control system to regulate the upper internal vapor pressure and lower internal vapor pressure of the retort apparatus thereby preventing the escape of significant quantities of hydrocarbon vapors which have been separated from the oil shale during retort treatment and at the same time preventing the contamination of the recovered hydrocarbon vapors with air which consists primarily of nitrogen, oxygen, and CO₂.

Another object of this invention is to provide an improved retort apparatus for separating hydrocarbons from oil shale, in which a cracking and distillation zone is constructed in such a manner that the temperature of the oil shale can be raised by means of an auxiliary heat source to a desired, necessary critical temperature sufficient to separate hydrocarbons in the vapor state from the organic matter in the oil shale while the oil shale is moving by gravitational force through the apparatus.

It is a still further object of the present invention to provide an improved retort apparatus for separating hydrocarbons from crushed oil shale in which an auxiliary heat source is utilized for raising the oil shale in the cracking and distillation zone to the critical temperature for separating the hydrocarbons in vapor form from the organic matter during gravitation movement of the crushed oil shale, and a separating means is disposed in communication with the cracking and distillation zone for withdrawing the hydrocarbon vapors formed therein as a function of the pressure in the cracking and distillation zone and in the respective zones on opposite sides of the cracking and distillation zone in the retort apparatus.

It is a yet further object of the present invention to provide an improved retort apparatus for separating hydrocarbons from crushed oil shale in which the temperature gradient in the cracking and distillation zone is reduced to a low value.

It is a further object of the present invention to provide an improved retort apparatus for separating hydrocarbons from crushed oil shale in which heat exchange means in the preheat zone and waste heat recovery zone provide for the transfer of heat recovered in the waste heat recovery zone to the preheat zone.

With these and other objects in view the invention will be better understood by reference to the attached description of the apparatus and system in accordance with the present invention taken along with the Figures of the drawings.

DESCRIPTION OF THE FIGURES

FIG. 1 is a schematic front view of one form of retort apparatus and system for recovery of hydrocarbons from oil shale in accordance with the present invention.

FIG. 2 is a schematic view of the form of the invention shown in FIG. 1 turned 90°.

FIG. 3 is a top view of the apparatus and system shown in FIG. 1.

FIG. 4 is a cross-section taken on line 4--4 of FIG. 1.

FIG. 5 is a schematic view of the apparatus and system shown in FIGS. 1 and 2 with the cracking and distillation zone enlarged to more clearly show the elements and structure operatively associated with the auxiliary heating means and the portions and elements therein associated with the separating means for withdrawing hydrocarbon vapors released from the oil shale moving through the cracking and distillation zone in the apparatus.

FIG. 6 is an enlarged fragmentary perspective view of the lower portion of the cracking and distillation shown in FIGS. 2 and 5 showing the heat exchange members and the U-shaped venting members.

FIG. 7 is a fragmentary view of some of the heat exchange tubes and the transverse U-shaped venting members for evacuating the hydrocarbon vapors from the cracking and distillation zone.

FIG. 8 is an enlarged view of one of the U-shaped venting members for evacuating hydrocarbon vapors from the cracking and distillation zone.

FIG. 9 is an enlarged side view of the control assembly for opening and closing the outlet end of the retort apparatus shown in FIGS. 1, 2 and 5 of the drawings, shown in the open position.

FIG. 10 is a fragmentary enlarged view of the control assembly shown in FIG. 9 showing the outlet port closure members in the closed position.

FIG. 11 is a schematic elevational view of a retort apparatus according to another embodiment of the present invention.

FIG. 12 is a part vertical diagram of a portion of the cracking and distillation zone of the retort apparatus of FIG. 11.

FIG. 13 is a cross-sectional diagram of the portion of the cracking and distillation zone of FIG. 12, taken along lines 13--13 thereof.

FIG. 14 is a schematic diagram of the arrangement of the heat exchange tubes in the cracking and distillation zone of FIG. 12, used for illustrating the area occupied by each heat exchange tube in cross-section.

FIG. 15 is a cross-sectional view taken along lines 15--15 of FIG. 11, showing of the coil arrangement in the preheat zone.

FIG. 16 is a cross-sectional view of the coil arrangement of FIG. 15, taken along lines 15--15 thereof.

DESCRIPTION OF THE PREFERRED EMBODIMENTS FIRST EMBODIMENT

Referring to the drawings FIGS. 1 to 10 show one preferred retort apparatus and system in accordance with the present invention, for separating, vaporizing and recovering hydrocarbons from oil bearing ores such as oil bearing shales.

The system includes a storage hopper generally designated 1 from which crushed oil bearing shales are fed to the system. The oil bearing shales will be crushed by any suitable means such as a jaw crusher (not shown) to less than 3/4" in size before they are delivered to the storage hopper. This size for the oil bearing shale has been found suitable for use in the elongated housing or recovery tower generally designated 10 and more fully described hereinafter. However, if possible it is preferred to reduce the oil bearing shales to a size from small particles to less than 1/2" or in a range of sizes less than 1/2". Those skilled in the art will recognize that reducing the size of the oil shale is not only to increase the amount of surface that can be treated in the elongated housing or recovery tower 10 but in addition to aid or to favor gravity flow movment of the oil shale through the apparatus.

With a jaw crusher, approximately one-sixth of the crushed oil shale will be made of fines. The use of crushed oil shale is preferable to ground oil shale which contains approximately 50% fines, and which results in a health hazard from fines in the atmosphere and a danger to the operation of the machinery. It is, however, important that some fines be included as part of the oil shale, since fines prevent channeling of air through the apparatus and thereby keeps air out if the pressure drops. Accordingly, the present invention is particularly suited for operation with crushed oil shale.

The storage hopper 1 has a storage hopper inlet opening as at 2 for receiving the crushed or broken oil shale and a hopper outlet 3 at the lower end thereof communicates with screw conveyor inlet 4 on the screw conveyor 5 connected to the storage hopper 1 about the hopper outlet 3. Screw conveyor 5 is a device for longitudinally transferring crushed solids and there are many conventional designs for this purpose easily purchaseable on the open market. Therefore this device will not be more fully described herein.

The screw conveyor 5 at the end remote from the screw conveyor inlet 4 is provided with a screw conveyor outlet 6 disposed to deliver the crushed oil shale to the upper or inlet end 7 of the elongated housing or recovery tower 10.

In the hopper 1 a control assembly 8 is connected with a sensing arm 8a which responds to the level of the crushed or broken oil shale in the hopper to signal operation of the motor 8b for driving the conveying bucket assembly 8c to supply crushed oil shale in accordance with the level of crushed oil shale in the hopper 1.

Similarly in the upper end 7 of the elongated housing or recovery tower 10, a similar control assembly 9 is connected with a sensing arm 9a which responds to the level of the crushed or broken oil shale in the upper end of the housing or tower 10 to signal operation of the motor 9b for driving the screw conveyor 5 to deliver the crushed or broken oil shale through the opening 6 into the upper end 7 of the housing or tower 10.

The movement of the crushed oil shale through the housing or tower 10 will be regulated and controlled by an outlet or exit control assembly generally designated 20 more fully described below. However, it is thought to be clear that the respective delivery of crushed oil shale to the upper end 7 of the housing or tower 10 and into the hopper 1 will be a function of and are operatively related to the movement of the crushed oil shale as regulated and controlled by the outlet or exit control assembly 20.

ELONGATED HOUSING OR RECOVERY TOWER

The elongated housing 10 includes side walls as at 11a, 11b, 11c and 11d and a top or cover member 12. The side walls 11a, 11b, 11c and 11d are shaped and sized preferably square in cross-section and define from the inlet or upper end to the outlet or lower end thereof a transfer passage 13 for crushed oil shale.

The elongated tower side walls are made of conventional steel and the walls may be insulated as shown by the phantomized lines 15 to conserve heat loss therethrough.

The side walls may be built in sections and joined by suitable flange means as at 15a, 15b, 15c and 15d etc. to permit the sections to be bolted, welded or otherwise joined together in any conventional manner, as will be understood by those skilled in the art.

As is shown in FIGS. 1, 2, 5, 9 and 10 the end of the elongated housing or recovery tower 10 is provided with an outlet 16 which is in turn communicated with a plurality of elongated cone shaped outlet port members 17 respectively provided with outlet ports as at 17a, 17b and 17c etc. as shown in FIGS. 9 and 10.

Thus crushed oil shale will pass from the outlet 16 through the outlet port members 17 to the outlet ports 17a, 17b, 17c, etc.

Discharge of the crushed oil shale from each of the outlet ports 17a, 17b, 17c, etc. is controlled by an elongated arcuate shaped member or closure head 18 which is pivotally connected as at 18a and 18b on opposite ends of each respective outlet port member 17 so that the arcuate shaped member or closure head 18 may be pivoted to the open position shown in FIG. 9 from the normally closed position shown in FIG. 10.

It is particularly noted that the arcuate shape of the member or closure head 18 is so designed that in the closed position as shown in FIG. 10 there will be a clearance as at 18c between the outlet ports 17a, 17b, 17c etc., and the inner arcuate face of the respective arcuate members on closure heads 18 as is shown in FIG. 10. This arrangement in the closed position permits the crushed oil shale to compress between the outlet ports 17a, 17b, 17c, etc., and the inner face of the closure heads 18 without spilling over and enables the closure heads 18 on opening movement to wipe the outlet port clear so that the crushed oil shale will move freely from the outlet ports 17a, 17b, 17c, etc., when the closure head is in the open position.

Further, the arcuate shape of the closure heads 18 are so defined with respect to the pivotal point 18a that automatic stop limits are provided for the closure heads 18. Thus, on the closing movement one end of the closure head 18 will contact the outer wall 19a of the next adjacent outlet port member and on opening movement thereof the opposite end will contact the same outer wall of the outlet port member on which it is pivotally connected as is shown at FIGS. 9 and 10 of the drawings.

The operation or movement of the arcuate members or closure heads 18 are controlled by the outlet control assembly 20 which includes lever arms 21 connected at one end to the arcuate members or closure heads 18 and at the opposite end to an actuating rod assembly 22.

Any suitable type of pivotal arrangement can be used for this purpose. In the arrangement shown the lever arms 21 are pivotally connected at both ends. Between the actuating rod assembly collars 22a and 22b springs 22c are disposed between the pivoted end connections for the lever arm 22.

The actuating rod assembly 22 is moved by a suitable motor 22d which is in turn operated by signals from a timer 22e so that the actuating rod assembly will move in one direction to maintain the closure head 18 in the closed position as shown in FIG. 10 for about 10 seconds and then in the opposite direction to the open position shown in FIG. 9 where it will remain for about 5 seconds.

During the period when the closure head is in the open position, crushed and broken oil shale will discharge from the outlet ports 17a, 17b, 17c, etc. onto the belt 23a of any suitable type of conveying assembly generally designated 23.

Conveying assemblies for removing solid material are well known in the art and accordingly will not be more fully described.

The need for regulating and controlling the gravitional movement of the crushed or broken oil shale through the passage 13 in the elongated housing or recovery tower 10 is to permit the desired dwell time in the various operatively associated heat exchange zones which are established in the elongated recovery tower 10 so that the optimum recovery of hydrocarbon vapors from the crushed oil shale will be effected to provide an efficient oil recovery apparatus and system.

Thus, elongated recovery housing 10 and the transfer passage 13 formed therein are divided into four operatively associated zones hereinafter more fully delineated for treating the crushed oil shale as it moves gravitationally downward through the transfer passage 13. These zones are established by heat exchangers which are connected serially in the elongated housing so as to extend transversely of the transfer passage 13 in their respective zones.

Thus, in accordance with the method and process of the present system the crushed oil shale is first passed through drying zone 25 to substantially drive off or separate water in vapor form and non-condensible gases. Adjacent to and following the drying zone is a preheat zone 26 where the temperature of the crushed oil shale is raised to about 800°-825° F. (425°-475° C.).

The upper or preheating zone 26 extends from the drying zone in the elongated housing 11 to an intermediate or cracking and distillation zone 27 in the medial section of the transfer passage 13 in the elongated housing 10. In the cracking and distillation zone the temperature of the crushed oil shale is raised to the critical temperatures for cracking or decomposing the organic matter or kerogen, about 800°-1100° F. (425°-600° C.) into hydrocarbon vapors so that suitable separating means can be provided to remove the vaporized hydrocarbons and condense the same to the liquid phase.

Associated with the upper or preheating zone 26 is the lower or waste heat recovery zone 28 which extends from the lower end of the cracking and distillation zone to the outlet control assembly 20 connected to the discharge outlet 16 for the elongated housing or elongated recovery tower 10.

The heat needed to drive off the water and non-condensible gases in the drying zone 25 is accomplished by heat exchange across the heat exchanger tubes 25a, 25b and 25c utilizing a gaseous heat exchange medium vented from an auxiliary heating unit 50 for the cracking and distillation zone 27 as is shown in FIGS. 1 and 2 of the drawings and more fully described below.

The delivery of heat to the crushed oil bearing shale in the preheating zone 26 is accomplished by heat exchange with suitable fluid circulated through heat exchange tube bundles as at 26a, 26b, 26c, 26d and 26e which are transversely and serially mounted in spaced and interconnected relationship along the vertical or longitudinal line of the preheating section 26 in the transfer passage 13 as is shown in FIGS. 1 and 4 of the drawings.

Similarly, the transfer or withdrawal of heat from the spent oil shale when it leaves the intermediate or cracking and distillation zone 27 and moves downwardly through the waste heat recovery section 28 is also accomplished by means of heat exchange wherein heat is delivered to fluid circulating through the heat exchange tube bundles as at 28a, 28b, 28c, 28d, 28e, 28f, 28g, 28h, 28i and 28j which are transversely and serially mounted in spaced and interconnecting relationship along the vertical or longitudinal line of the waste heat recovery section 28 of the transfer passage 13 in the elongated housing 10 as is also shown in FIG. 1 of the drawings.

The waste heat recovery zone 28 is brought into operative association with the preheating zone 26 so that the waste heat recovered in the waste heat recovery zone can be used to preheat the entering crushed oil shale by means of any suitable type of pumping circuits generally designated 30 and 31 which can be used to interconnect the respective heat exchange tube bundles 28a to 28g of the waste heat recovery zone 28 with the heat exchange tube bundles 26a to 26e of the preheating zone 26. Thus, when the pumping circuit is in operation the desired heat exchange fluid can be circulated from one zone to the other to recover the waste heat and thus increase the efficiency of this system.

Further however, it will be noted that the pumping circuit must be adapted to pump a fluid between the heat exchanger tubes in the waste heat recovery section and the preheating section to achieve the desired operating temperatures for the system. Thus fluids must be utilized in the pumping circuits 30 and 31 such as heat transfer oil or silicone fluid that can withstand the waste heat temperatures of 800°-825° F. (425°-475° C.).

Referring to FIG. 1, the pumping circuit 30 is shown to include a common delivery line manifold 32 and a common return line manifold 33. Delivery line 32 is connected to the upper end of the serially connected heat transfer tubes 28a to 28d of the waste heat recovery section and the opposite end of the common delivery line 32 is connected to the lower end of the serially connected heat exchange tube bundle 26d and 26e of the preheating section 15.

The upper end of the heat exchange tube bundle 26d and 26e is in turn connected to one end of the common return line 33, the remote end of which is connected to a storage and accumulator member 34 to provide a source of heat transfer oil for the circulating pump 35 for the pumping circuit 30. Pump 35 has its suction 36 connected as by suction line 37 to the lower end of the storage and accumulator chamber 34 and the discharge 38 is connected by line 39 to the lower end of the waste heat exchanger tubes 28a to 28d.

Similarly in the pumping circuit 31 the common delivery line 40 is connected at one end to the upper end of the serially connected waste heat exchanger tubes 28e to 28g and has its remote end connected to the lower end of the preheat exchanger tubes 26a to 26c. The upper end of the serially connected preheater zone heat exchange tubes 26a to 26c is connected to the common return line manifold 41 the opposite end of which is connected to the storage accumulator 42 for providing a source of silicone fluid for the circulating pump 43. Circulating pump 43 has its suction 44 connected by suction line 45 to the lower end of the silicone storage and accumulator 42 and its discharge 46 connected by line 47 to the lower end of the serially connected waste heat exchange tubes 28e to 28g.

When the system is in operation the circulating pumps 35 and 43 will be placed in operation so that the respective pumping circuits 30 and 31 can deliver the waste heat from the waste heat recovery zone to the preheat zone in the elongated housing or recovery tower 10 so as to preheat the gravitational moving oil shale by the recovered waste heat which is therefore not lost during the operation of the system thus increasing the efficiency of the system.

In the gravitational movement of the crushed oil shale through the transfer passage 13 the crushed oil shale moves from the preheating zone 26 into the intermediate cracking and distillation zone 27 where the temperature is raised also by a heat exchange mechanism hereinafter described as the critical temperature required to decompose the organic matter or kerogen and thus separate and vaporize the oil in the crushed oil shale as it moves through this cracking and distillation zone 27.

The heat exchange mechanism consists of a plurality of serially connected tube bundles as at 27a, 27b, 27c, in the upper or first section and 27d, 27e and 27f in the lower or second section of the cracking and distillation zone which are mounted on the elongated housing 10 transversely to the longitudinal line of the transfer passage 13. However it will be noted that the heat exchanger tubes 27a through 27f are disposed at 90° to the heat exchanger tubes for the respective drying zone 25, preheat recovery zone 26 and waste heat recovery zone 28 because this heat exchanger mechanism in the elongated or recovery tower 10 is connected to an auxiliary heat supply assembly generally designated 50 which is connected exterially of the wall means 11b as is shown in FIGS. 2 and 3 of the drawings. The position of such auxiliary heat assembly permits a suitable separation means generally designated 60 to be connected to the side wall 11c of the elongated housing or recovery tower 10 so as to communicate with the respective upper seciton and lower section of the cracking and distillation zone to withdraw released hydrocarbons and other gases from the cracking and distillation zone as will be more fully described below.

The auxiliary heating assembly 50 provides hot combustion gases as the heat exchange medium to be passed through the heat exchange mechanism in the upper section and lower section of the cracking and distillation zone 27 and such hot combustion gases may be obtained from any suitable source such as a gas or oil burner generally designated 51. Auxiliary heating assemblies of this type are well known. The gas or oil burner 51 has a combustion chamber 52 with a combustion gas outlet 53 connected to the suction inlet 54 of a blower 55. The discharge 56 of the blower communicates by auxiliary heat delivery line 57 to the lower end of the lower section of the cracking and distillation zone 27. Since the lower section is serially connected to the upper section, the combustion gases pass through the lower section and the upper section and exit through the delivery line 58 to a vent line 59. In the vent line 59, a heat exchange coil 60 is mounted in any suitable manner. Heat exchange coil 60 is connected by inlet line 60a to the lower end of the serially disposed heat exchanger tubes 25a, 25b, and 25c in the drying zone 25 so that a heat exchange medium such as water and glycol can be passed thereto by any suitable type of circulating pump 60b which takes its suction from the accumulator 60d communicating with the return line 60c for returning the heat exchange medium to the heat exchange unit 60. Thus, waste heat is utilized for drying the incoming crushed oil shale as it moves gravitationally from the inlet end 7 downwardly through the transfer passage 13 in the elongated housing or recovery tower 10. The spent combustion gases will be vented to atmosphere. Any suitable means can be provided to reduce any harmful effect to the environment that might be caused by venting these combustion gases to the local atmosphere surrounding the retort apparatus and system in accordance with the present invention.

The addition of the heat which is supplied to the crushed oil shale moving through the cracking and distillation zone will raise the temperature of the crushed oil shale to the critical temperature required to decompose the organic matter or kerogen therein. This will cause the hydrocarbons to separate from the organic matter or kerogen and in accordance with the present invention a suitable separation means is provided for this purpose.

Thus referring to FIGS. 1, 2, 5, 6, 7 and 8 the cracking and distillation zone is shown to include a plurality of serially disposed vent members which are mounted in the elongated housing 10 transversely of the transfer passage 13 at 90° to the horizontal line of the heat exchanger tubes 27a to 27d in the respective upper and lower sections of the cracking and distillation zone and in alternate levels therewith as is shown in FIGS. 1, 5, 6 and 7 of the drawings.

The vent members 61a to 61h are U-shaped in cross-section and when connected in the housing are disposed to have the open end of the U inverted to face in a downward direction so that by normal expansion the hydrocarbon vapors will collect and enter the open mouth end of the U-shaped vent members 61a to 61f.

The U-shaped vent members 61a through 61h are connected at one end by bracket members 61i on each of the vent members to the lower edge of the openings 61j formed in the side wall 11c and by a support bracket 61k on the inner face of the side wall 11a so that the lower half of the U-shaped vent members 61a to 61h are blocked off and only the upper half communicates through the opening formed as at 61i thereon with the opening 61j in the side wall 11c so that each of the U-shaped vent members 61a, 61b, 61c and 61d communicate with the upper chamber 62 formed in the upper hydrocarbon collecting manifold 63 and each of the U-shaped vent members 61e, 61f, 61g and 61h communicate with the lower chamber 64 formed in the lower hydrocarbon collecting manifold 65 all of which is shown in FIGS. 6, 7 and 8 of the drawings.

The blocking off of the lower half of the inverted U-shaped vent members acts to prevent fines, particles or dust from the gravitationally moving crushed oil shale from rising up through the mouth of and into the inverted U-shaped vent members and therefore does not interfere with the free movement and collecting of the hydrocarbon vapors and other gases drawn by the hydrocarbon collecting manifolds 63 and 65. This also prevents contamination of these collected vapors and gases by the fines, dust and particles that may be present in the crushed oil shale.

The upper collecting manifold 63 and lower collecting manifold 65 in turn communicate through the respective connecting conduits 66 and 67 with the suction inlets respectively at 68 and 69 on the vacuum pumps 70 and 71 so that a suitable vacuum pressure may be maintained in the cracking and distillation zone 27 during the operation of the retort apparatus and system in accordance with the present invention.

The discharge outlets 72 and 73 of the vacuum pumps 70 and 71 communicate respectively through connecting pipes 74 and 75 to a common delivery manifold 76 which delivers the hydrocarbon vapors and other gases to the condenser 77 where the hydrocarbon vapors are condensed and discharged through drain 78 to a suitable point of storage, not shown, and the uncondensed gases are vented through a vent line 79 to a suitable point of collection or use as the case may be.

Since the elongated housing or recovery tower 10 is open to atmosphere at the respective upper or inlet end 7 and the lower or outlet end 20, those skilled in the art will readily recognize that the separated and vaporized mixture of hydrocarbon and gases formed in the intermediate cracking and distillation zone 27 must be protected from contact with oxygen in the atmosphere on the one hand and the environment must be protected from the pollution that would be caused by leakage of this mixture of hydrocarbon and other gases.

This is accomplished in the present invention by controlling the relative pressure in the transfer passage 13 on opposite sides of the cracking and distillation zone 27 as the crushed oil shale moves from the upper or inlet end 7 to the lower or outlet end 20 of the transfer passage 13.

Thus by reference to FIG. 1, the separation zone is shown to include control louvers as at 81 and 82 in the respective connecting passages of the conduits 66 and 67 which communicate with the respective suction inlets 68 and 69 of the pumps 70 and 71.

The operation of these pumps is controlled by the respective controllers as at 83 for the control louver 81, and at 84 for the control louver 82. Controllers 83 and 84 are operable responsive to an upper sensing means 85 for controlling louver 81 as a function of the pressure at a point between the drying zone 25 and preheat zone 26 and a lower sensing means 86 which actuates the controller 84 as a function of the change in pressure at a predetermined point in the waste heat recovery zone spaced from the discharge outlet 20 of the elongated housing or recovery tower 10.

The sensing mechanism 87 on the upper sensing means 85 will be set to maintain a pressure in the elongated housing or recovery tower 10 just above atmospheric pressure so as to prevent any mixture of air from leaking or flowing towards the intermediate cracking and distillation zone 27. Similarly the sensing mechanism 88 on the lower sensing means 86 will be set above atmospheric pressure so as to prevent any air from leaking inwardly from the discharge outlet 20 into the waste heat recovery zone. As an example, an approximate measure of atmospheric pressure at 6000 feet above sea level is a level of 275" in a water column. The pressures in the zones surrounding the cracking and distillation zone may be maintained at a pressure equivalent to 2751/2" in a water column.

The vacuum pumps 70 and 71 will be operated at a pressure substantially above atmospheric pressure because of the volume of gases which are produced in the cracking and distillation zone and the control louvers 81 and 82 will be so actuated by the control means above described that they will maintain a pressure above atmospheric pressure and above the pressures sensed by sensing mechanisms 87 and 88 in the cracking and distillation zone at all times when the retort apparatus and system in accordance with the present invention is in operation. For example, the pressure in the cracking and distillation zone may be equivalent to 276" in a water column.

In the event that there is any leakage of the hydrocarbon and gas mixture from the cracking and distillation zone, the same will flow upwardly through the elongated housing or recovery tower 10 into the space 90. The moisture separated from the drying section and miscellaneous loose fines will pass upwardly through the connecting passage 91 to a vent condenser 92 where the moisture will be condensed and the non-condensible gases, the fines, dust, etc. will be vented through the vent 93 to atmosphere. The water obtained by condensing the moisture is sprayed on the spent shale exiting from the apparatus to prevent dust storms.

In the present invention it is necessary to also facilitate movement of the crushed oil shale through the elongated housing or recovery tower 10 from the inlet end of the recovery tower 10 to the outlet end thereof.

Attention is therefore particularly called to FIG. 1 of the drawings which shows that the fins 93 on tubes 25a, 25b, etc. in the drying zone 25; the fins 94 on the tubes 26h and 26i in the preheating zone 26, and the fins 95 on the tubes 28a, 28b, etc. in the waste heat recovery zone 28 are in substantial alignment with each other in assembled position.

This construction when coupled with the non-finned heat exchanger tubes 27a, 27b, etc. in the cracking and distillation zone 27, the relatively slippery or low friction characteristic of the crushed oil shale, and the operation of the system under anaerobic conditions enables the crushed oil shale to slide or sift with relative ease through the recovery tower 10 on movement of the outlet control assembly 20 in intimate heat exchange relation with the finned and non-finned tubing so that the heat will be conductively transferred substantially uniformly through the packed mass of the crushed oil shale as it moves through the recovery tower 10.

The fins on the finned tubes in the drying zone, preheat zone and waste heat recovery zone are aligned and generally spaced in the horizontal plane approximately 1" from each other.

Finned tubes are used in the drying zone 25, preheat zone 26 and waste heat recovery zone 28 because the heat exchange medium is a liquid, non-finned and oval shaped tubes are used in the cracking and distillation zone 27 because the heat exchange medium is a gas. The use of finned and non-finned oval tubes in this manner increases the heat exchange efficiency of the apparatus and process in accordance with the present invention.

Further in regard to facilitating movement of the crushed oil shale through the elongated housing or recovery tower 10, this apparatus provides a relatively simple visual inspection test to determine whether the crushed oil shale is flowing with relative freedom through the elongated housing or recovery tower 10. Thus, because of the outlet port member 17 and the outlet ports 17a, 17b, 17c etc. when the outlet control assembly is moved to open position, the operator can visually observe whether the crushed oil shale is discharging uniformly from the outlet control assembly by the size and shape of the piles of crushed oil shale delivered onto the conveyor belt 23a.

In the event that the outlet control assembly 20 indicates non-uniform delivery of the spent crushed oil shale from the elongated housing or recovery tower 10, any suitable convenient device such as a vibrating mechanism, not shown, or elongated agitating rods extending end to end through the tower, not shown, may be used to relieve any local portion in the mass of moving crushed oil shale where undue compression or clogging has occurred.

The construction of the vent members and the operation of the system will be such that it will avoid an excessive pressure drop and while the vent members 61a, 61b, 61c, etc. are shown as opening on only one side of the elongated housing or recovery tower 10, those skilled in the art will readily recognize that the vent members could open on opposite sides of the recovery tower 10 and by suitable manifolding passed to the common collecting ducts 62 and 63 so as to provide the required drawing off of recovered hydrocarbon vapors to provide a proper balance and pressure drop in this area of the system.

Operation

In operation, with the outlet control assembly 20 in the closed position, the crushed oil shale is delivered from the hopper 1 by the screw conveyor 5 to the inlet 7 of the transfer passage 13 in the elongated housing 10 until the entire transfer passage 13 is completely filled with the crushed oil shale from the inlet 7 to the outlet 16 thereof.

The auxiliary heating assembly 50 is now placed into operation by igniting the oil or gas burner 61 and combustion gases will be passed by the blower 55 to the respective lower and upper sections of the cracking and distillation zone 27. The combustion gases passing through the heat exchange tubes 27a to 27e will raise the temperature of the crushed oil shale sufficiently to cause decomposition of the organic matter or kerogen in the crushed oil shale so as to release hydrocarbon vapors and other gases therefrom.

The separation system 60 is placed into operation by turning on the vacuum pumps 70 and 71 and the hydrocarbon vapor and other gases will be drawn from the cracking and distillation zone to the collecting chamber 62 and 64 through the U-shaped vent members in communication therewith. The released and recovered hydrocarbon vapors and other gases will be pumped by the vacuum pumps 70 and 71 through the connecting lines 74 and 75 to the common return or delivery line 76 into the condenser 77 where the hydrocarbon vapors and other gases will be condensed and passed to storage through the drain line 78, as soon as condensing occurs and hydrocarbons are being recovered. The timer 22e and motor 22d are turned on to actuate the outlet control assembly 20 and this will commence the gravitational movement of the crushed oil shale at an approximate rate of about 1' per minute through the transfer passage 13.

As the crushed oil shale begins to move through the transfer passage 13, the conveyor 5 will simultaneously be turned on to deliver crushed oil shale to the inlet end 7 of the transfer passage. The control units 8 and 9 will operate to pass the crushed oil shale into the inlet end 7 of the transfer passage 13 so that it is uniformly distributed across the transverse cross-section of the elongated transfer passage 13. The operation of the conveyor 5 will automatically coordinate with the outlet control assembly 20 which is operated as a function of the rate of recovery of hydrocarbon vapors from the cracking and distillation zone 27.

As the hydrocarbon vapors and other gases are pumped from the cracking and distillation zone 27 the control louvers 81 and 82 which will be normally open will be slowly moved to a position by the controllers 83 and 84 which will correspond to the predetermined pressure sensed by the sensing mechanisms 87 and 88 in the respective heat zones and waste heat recovery zones of the elongated housing or recovery tower 10 such that the pressures therein will continue to be maintained at pressures above atmospheric pressure at a point such that little or no leakage of the hydrocarbon vapors or other gases will occur through the respective preheat zones and waste heat recovery zones of the elongated housing or recovery tower 10.

Thus the operation of the system will continue substantially free of any atmospheric oxygen with the dangers that might occur by reason thereof.

Second Embodiment

Referring now to FIGS. 11 to 16, there is shown a retort apparatus and system in accordance with another embodiment of the present invention, for separating, vaporizing and recovering hydrocarbons from oil bearing ores such as oil bearing shales. The apparatus of FIGS. 11 to 16 constitutes a modification of the retort apparatus of FIGS. 1 to 10, with the basic structure and operation being the same, and accordingly, much of such basic structure is omitted herein for the sake of brevity.

As shown in FIGS. 11-16, raw oil shale enters the elongated housing 110 formed with side walls 111a, 111b, 111c and 111d, at the upper end thereof, preferably in the same manner as that taught in the first embodiment of FIGS. 1 to 10. Housing 110 forms, in sequence, from the upper end thereof, a drying-zone 125, a preheating zone 126, a cracking and distillation zone 127 and a waste heat recovery zone 128.

In accordance with the second embodiment of the present invention, hot gases are used in the cracking and distillation zone to raise the temperature of the oil shale sufficiently to crack or decompose the organic matter or kerogen into hydrocarbon vapors for removal therefrom.

In this regard, a plurality of banks of heat exchange tubes 227 are positioned within cracking and distillation zone 127 and extend through opposing side walls 111b and 111d of tower 110, as shown in FIGS. 11 and 13. Each bank is, in a preferred embodiment, comprised of eight vertical rows of heat exchange tubes 227, with each bank of eight rows being separated by a transverse row of U-shaped vent members 161 for removal of the separated hydrocarbon vapors.

The heat exchange tubes 227 in each row are staggered in relation to the heat exchange tubes of adjacent rows, as shown in FIG. 12. The reason for staggering the heat exchange tubes between adjacent rows is to provide a convoluted flow of crushed oil shale through the cracking and distillation zone 127 so as to control the speed of movement of the crushed oil shale through cracking and distillation zone 127 also thereby provide for maximum heat transfer with heat exchange tubes 227.

In accordance with an important aspect of the second embodiment of the present invention, each of the heat exchange tubes 227 has an oval or elongated configuration, as shown in FIGS. 12 and 14. The reason for providing such oval configuration is to reduce the temperature drop of heated air through the tubes in the cracking and distillation zone 127 that would otherwise be relatively large with the use of circular heat exchange tubes. In other words, oval or elongated heat exchange tubes 227 result in a greatly increased surface area which reduces the aforementioned temperature drop in the cracking and distillation zone. As shown in FIG. 14, each heat exchange tube 227, in cross-section, occupies approximately one-third of the area XY. The area XY constitutes the surrounding area for heat exchange tubes 227, in cross-section, which is not related with any other heat exchange tube. With circular heat exchange tubes, the corresponding area occupied by the tube is approximately only twelve percent, resulting in a greatly reduced efficiency and a larger temperature drop of heated air therethrough. Further, by use of the oval or elongated heat exchange tubes 227, the necessity of providing fins to enhance the heat exchange capability of the tubes is eliminated, although such fins may be provided, if desired.

In a preferred embodiment, heat exchange tubes of the same row have a minor outside diameter of 1 1/16" and are separated from adjacent heat exchange tubes 227 of the same row by 15/16". In addition, heat exchange tubes of one row are separated from heat exchanger tubes of an adjacent row, preferably by a distance of 3/4", but no greater than 7/8".

As shown in FIG. 11, a gas burner 150 supplies a heated gas, such as air, to a fan or blower 155 which, in turn, forces the heated gas through the heat exchange tubes 227 of a first or lowest section 127a of cracking and distillation zone 127 through an input manifold 156.

The gas passing through the heat exchange tubes 227 exits at the opposite end thereof into a connecting manifold 157 which connects a second higher level section 127b in the cracking and distillation zone 127. Thus, the gas entering manifold 157 travels upwardly, as shown by the arrows in FIG. 11, and is forced through heat exchange tubes 227 of the higher level section of cracking and distillation zone 127. The gas exiting from these latter tubes 227 enters an exit manifold 158 and returns through a return conduit 159 to the input of blower 155. In addition, or alternatively, the gas or a portion thereof from exit manifold 158 may exit the apparatus through a vent 160 having a controllable butterfly valve 162 pivotally connected within vent 160, as at 163. Control of butterfly valve 162 may be performed manually, or may be automatically controlled dependant upon the temperature of the heated gas entering the cracking and distillation zone 127, for example, measured within input manifold 156.

Although FIG. 11 shows cracking and distillation zone 127 separated into only two sections, an upper section 127b and a lower section 127a, cracking and distillation zone 127 is preferably separated into a plurality, such as eight, vertically oriented sections. In this manner, a plurality of gas burners 150 and blowers 155 are provided. Only two sections of cracking and distillation zone 127 have been shown in FIG. 11 for the sake of brevity and ease of understanding the present invention.

In accordance with the second embodiment of the present invention, heat recovered from the waste heat recovery zone 128 is transferred to preheating zone 126 to preheat the incoming oil shale.

In this regard, a closed loop heat exchange system is provided. In particular, preheating zone 126 is formed with a heat exchanger coil arrangement, as shown in FIGS. 15 and 16, the coil being arranged generally transverse to heat exchange tubes 227 of cracking and distillation zone 127. In the arrangement shown in FIGS. 15 and 16, the heat exchanger coil 325 is formed in a tortuous or zig-zag path, in each of a plurality of vertical rows 326a, 326b . . . 326N. More particularly, the heat exchanger coil 325 extends in a zig-zag path in the uppermost row 326a, then follows a zig-zag path in the adjacent, next lower row 326b, and so on. Alternate rows 326a, 326c, 326e . . . are in line, but are offset or staggered with respect to the remaining alternate rows 326b, 326d, 326f . . . to obtain maximum heat exchange efficiency.

As shown in FIGS. 11 and 15, the heated fluid enters the lowermost row 326N formed by coil 325 through input pipe 327 and travels in the zig-zag or tortuous path of such row. Thereafter, the fluid travels to the next upper, adjacent row 326 (N-1) and travels in a zig-zag path therein, and so on, until the fluid reaches the uppermost row 326a where it exits through exit pipe 328. Arrows have been provided in FIG. 15 to show the manner of flow of heated fluid through coil 325 in preheating zone 126.

In order to further enhance the heat transfer in preheating zone 126, fins 334 are provided along coil 325 for each row 326a, 326b . . . 326N. More particularly, as shown in FIG. 16, fins 334 are in the form of elongated sheet metal sections and extend in a direction transverse to the longitudinal direction of coil 325 in each row, and extend end to end in contact with the inner surface of walls 111b and 111d of tower 110. The fins 334 of each vertically arranged row 326a, 326b . . . 326N are aligned with corresponding fins in adjacent rows in the vertical direction so as not to hinder the flow of crushed oil shale through the tower.

As shown in FIG. 15, a plurality of fins 334 are provided for each row of coil 325 to provide maximum heat exchange efficiency.

With the arrangement of fins 334, as above described, it is also possible to use a vibrating assembly (not shown) with one or both of side walls 111b and 111d to vibrate fins 334, and thereby heat exchanger coil 325, to remove any oil shale that may settle thereon. The vibrating assembly may take any suitable form to provide a continuous small vibration to the side walls, or even provide periodic impact forces to these side walls. Alternatively, the user can manually vibrate the side walls by any suitable means.

Although not shown, the heat exchange coil arrangement in waste heat recovery zone 128 is substantially identical to that in preheating zone 126, as shown in FIGS. 15 and 16.

In accordance with the second embodiment of the present invention, oil is pumped by means of an oil pump 329 through the heat exchange coil in waste heat recovery zone 128. The oil recovers heat from the spent oil shale and then travels to an oil heater 330 which further heats the oil, whereupon the heated oil is transferred through heat exchanger coil 325 in preheating zone 126 to preheat the incoming raw oil shale. The oil exiting from heat exchange coil 325 enters an air eliminator 331 which eliminates air in the oil and transmits the resultant oil back to oil pump 329 of the closed loop system. In addition, an expansion tank 332 is provided in conjunction with air eliminator 331, as shown in FIG. 11.

Having described specific preferred embodiments of the invention with reference to the accompanying drawings, it is to be understood that the present invention is not limited to those specific preferred embodiments, and that various changes and modifications may be effected therein by one of ordinary skill in the art without departing from the spirit and scope of the present invention as defined by the appended claims. 

What is claimed is:
 1. A retort apparatus for recovering hydrocarbons from oil shale comprising:a. an elongated housing, having passage means end to end therethrough, inlet means to permit delivery of crushed shale into one end of the housing for movement along said passage means, and outlet means in communication with the end of the passage means remote from the inlet means for removing the spent oil shale from the passage means, said passage means disposed serially between the inlet means and the outlet means to define in the passage means a drying zone, a preheat zone, a cracking and distillation zone, and a waste heat recovery zone, b. a plurality of heat exchange means connected in said housing for heat exchange with the crushed oil shale moving through said passage means, c. circulating means connecting the respective one of said plurality of heat exchange means in the preheat zone with the respective one of said plurality of heat exchange means in the waste heat recovery zone for passing waste heat from said waste heat recovery zone to said preheat zone, d. auxiliary heating means connected to the one of said plurality of heat exchange means in said cracking and distillation zone to raise the temperature of the crushed oil shale moving therethrough to the critical temperature for separating hydrocarbon vapors from said crushed oil shale, e. said heat exchange means in the cracking and distillation zone including a plurality of parallel heat exchange tubes, each heat exchange tube having an elongated cross-sectional configuration, said heat exchange tubes being arranged in vertical rows, the heat exchange tubes in each row being staggered with respect to heat exchange tubes of adjacent vertical rows, each heat exchange tube, in cross-section, having an associated surrounding area not related with any other heat exchange tube, and the area of each heat exchange tube, in cross-section, defined by the external dimensions thereof, constituting approximately one-third of the associated surrounding area, f. separating means connected in said housing for communication with said cracking and distillation zone to withdraw and condense the hydrocarbon vapors released from the crushed oil shale moving through the passage means and to recover the same, g. means connected to the housing to control movement of crushed oil shale through said passage means, h. means for sensing the pressures in said passage means on opposite sides of said cracking and distillation zone, i. means for adjusting the pressure in said cracking and distillation zone in response to the sensed pressures and to a pressure greater than the pressures in the other zones, and j. means adjacent the outlet means for removing spent oil shale discharged therefrom.
 2. The retort apparatus as claimed in claim 1 including,a. means for delivering crushed oil shale to the inlet means in communication with the passage means in the elongated housing, and b. means in the elongated housing adjacent the inlet means for generally spreading the crushed oil shale uniformly across the transverse width of the passage means in the elongated housing.
 3. The retort apparatus as claimed in claim 1 including,a. means for delivering crushed oil shale to the inlet means in communication with the passage means in the elongated housing, b. said means including,i. conveyor means for the crushed oil shale, ii. hopper means for receiving the crushed oil shale from the conveyor means, and iii. screw conveyor means for delivering crushed oil shale from the hopper means to said inlet means.
 4. The retort apparatus as claimed in claim 3 including, means in the hopper means for controlling the operation of the conveyor means to deliver crushed oil shale to the hopper means.
 5. The retort apparatus as claimed in claim 3 including,a. first means in the hopper means for controlling the operation of the conveyor means to deliver crushed oil shale to the hopper means, b. second means connected in the inlet end of the passage means for the elongated housing for operating the screw conveyor means and for generally spreading crushed oil shale uniformly across the transverse area of the passage means, and c. said first means and said second means operative as a function of the operation of the means for controlling movement of the crushed oil shale through the passage means.
 6. The retort apparatus as claimed in claim 1 wherein the means to control movement of crushed oil shale through the passage means includes,a. a plurality of spaced outlet ports formed in the outlet means for the elongated housing, b. closure members pivotally connected on the elongated housing and disposed to normally maintain said outlet ports closed, and c. means for actuating the closure members to an open position to maintain said outlet ports open for a period of time to establish a predetermined rate of movement of the crushed oil shale through the passage means.
 7. The retort apparatus as claimed in claim 6 wherein the closure members have a predetermined clearance relative to the outlet ports to prevent the crushed oil shale from compressing and clogging in the outlet ports and to permit self-cleaning wiping action during movement of the closure members to the open position.
 8. The retort apparatus as claimed in claim 6 wherein,a. said closure members have an arcuate shape in cross-section, b. the closure members in the closed position have a predetermined clearance relative to the outlet ports to prevent the crushed oil shale from compressing and clogging in the outlet ports and to permit self-cleaning action by the closure members on opening movement thereof.
 9. The retort apparatus as claimed in claim 1 wherein the means to control movement of crushed oil shale through the passage means includes,a. outlet port means for the elongated housing, b. closure means pivotally connected on the elongated housing and disposed for movement to open and close the outlet port means to regulate movement of the crushed oil shale from the passage means in the elongated housing, and c. means for actuating the closure means to open and closed positions in a predetermined cycle to maintain movement of the crushed oil shale in the passage means at a rate of approximately 1 foot per minute.
 10. The retort apparatus as claimed in claim 9 wherein the actuating means includes,a. lever assembly means slidably connected to said elongated housing and pivotally connected to the closure means, b. a motor for moving the lever assembly means, and c. means for operating the motor to cause the motor to actuate the lever assembly means for holding the closure means open to produce said desired rate of movement of the crushed oil shale.
 11. The retort apparatus as claimed in claim 1 wherein said means for adjusting is operatively connected to the separating means and maintains a predetermined operating pressure in the preheat zone and the waste heat recovery zone to prevent separated hydrocarbon vapors from passing to atmosphere through the inlet means and outlet means for the elongated housing and to prevent the contamination of hydrocarbon vapors with nitrogen, air and CO₂ from the atmosphere.
 12. The retort apparatus as claimed in claim 1 including,a. a plurality of vent members mounted in said housing in the cracking and distillation zone thereof, b. each of said vent members disposed in spaced relation to each other and having at least one opening therein disposed for communication with the hydrocarbon vapors released from the crushed oil shale moving through said cracking and distillation zone, and c. said separating means including vacuum means connected to said vent members to draw off the hydrocarbon vapors entering the at least one opening in each of said vent members.
 13. The retort apparatus as claimed in claim 1 including,a. a plurality of vent members mounted transversely of the elongated housing in the cracking and distillation zone formed therein, and each of said vent members having a vent opening thereon, b. said transverse vent members being U-shaped in cross section and so connected in assembled position that the open U-shaped section is disposed at the lower portion to receive hydrocarbon vapors, and c. said separating means including vacuum means connected to the vent opening on each of said transverse vent members to draw off hydrocarbon vapors entering the open U-shaped section of said vent members.
 14. The retort apparatus as claimed in claim 1 including,a. a plurality of vent members mounted transversely of the elongated housing in the cracking and distillation zone formed therein, b. each of said transverse vent members having an opening at the upper section thereof, and an opening at the lower section for communication with the hydrocarbon vapors released from the crushed oil shale moving through said cracking and distillation zone, c. said separating means including vacuum means connected to the opening in the upper section of each of said transverse vent members to draw off the released hydrocarbon vapors, and d. said means for adjusting operatively connected to the separating means to regulate the operating pressure thereof and to maintain a predetermined pressure in the respective preheating zone and waste heat recovery zone in the elongated housing.
 15. The retort apparatus as claimed in claim 1 wherein,a. said cracking and distillation zone has an upper section and a lower section, b. said separating means includes first vacuum means communicating with the upper section of the cracking and distillation zone, and second vacuum means connected with the lower section of the cracking and distillation zone, c. said means for sensing includes first pressure sensing means connected in said preheat zone, and second pressure sensing means connected in said waste heat recovery zone, d. said first pressure sensing means operatively connected to said first vacuum means, and e. said second pressure sensing means operatively connected to said second vacuum means.
 16. The retort apparatus as claimed in claim 1 wherein, the separating means includes a condenser for condensing the hydrocarbon vapors separated from said cracking and distillation zone.
 17. The retort apparatus as claimed in claim 1 wherein,a. said auxiliary heating means includes a vent stack for combustion gases, and b. said vent stack is connected to the one of said plurality of heat exchange means in the drying zone for venting the combustion gases therethrough to dry the incoming crushed oil shale.
 18. The retort apparatus as claimed in claim 1 wherein,a. the plurality of heat exchange means in the drying zone, the preheat zone, and the waste heat recovery zone include heat exchange tubes having fins thereon, b. the fins on the heat exchange tubes for each of the plurality of heat exchange means disposed in alignment with each other in assembled position.
 19. The retort apparatus as claimed in claim 18 wherein the aligned fins on the respective heat exchange tubes are spaced in the horizontal plane approximately 1" from each other.
 20. The retort apparatus as claimed in claim 1 including, means for releasing clogged portions of the mass of gravitationally moving crushed oil shale.
 21. The retort apparatus as claimed in claim 1 including a vent condenser connected to the inlet end of said elongated housing for condensing hydrocarbon vapors leaking into the inlet end of the passage means formed in the elongated housing and for venting non-condensible vapors and gases collected in said passage means.
 22. The retort apparatus as claimed in claim 1 including a control assembly for regulating movement of said crushed oil shale from said outlet means comprising,a. closure means pivotally mounted on said housing for operative association with the outlet means to open and close the same, and b. means for actuating the closure means from an open to a closed position in accordance with a predetermined cycle to regulate the movement of the crushed oil shale in the housing.
 23. The retort apparatus as claimed in claim 22 wherein,a. said closure means is arcuate in cross-section, b. the closure means is disposed relative the outlet means to provide a small clearance therebetween in the closed position to prevent the crushed oil shale from compressing and clogging in the outlet means and to provide a self-wiping action on opening movement of the closure means.
 24. The retort apparatus as claimed in claim 22 wherein the means for actuating the closure means includes,a. lever assembly means slidably mounted on the housing and pivotally connected to the closure means, b. a motor for moving said lever assembly means to and fro to pivot the closure means between a normally closed position to an open position, and c. means for operating the motor in a predetermined cycle to regulate the discharge of the crushed oil shale in the housing to provide a desired predetermined movement therethrough of the crushed oil shale.
 25. The retort apparatus as claimed in claim 24 wherein the means for operating the motor is an electrical timing circuit.
 26. The retort apparatus as claimed in claim 1, wherein said housing has wall means defining said cracking and distillation zone and at least one opening formed in said wall means, and further comprising,a. an elongated U-shaped body connected between the wall means defining the cracking and distillation zone in said retort apparatus, b. said U-shaped body connected in an inverted position so that the open end of the U-shaped body faces downwardly in the assembled position, c. end plate means connected on at least one end of said U-shaped body having an opening therein, and bracket means formed thereon, and d. said bracket means disposed to mount the elongated U-shaped body in the cracking and distillation zone in the opening formed in said wall means so that the opening in the end plate will align with said at least one opening in the wall means.
 27. The retort apparatus as claimed in claim 1, wherein said heat exchange means in said preheat zone and said waste heat recovery zone includes heat exchange tubes having fins thereon.
 28. The retort apparatus as claimed in claim 27, wherein said heat exchange tubes in said preheat zone and said waste heat recovery zone are arranged in a plurality of vertical rows.
 29. The retort apparatus as claimed in claim 28, wherein said heat exchange tubes in each row are staggered with respect to heat exchange tubes of adjacent rows.
 30. The retort apparatus as claimed in claim 29, wherein the fins on the heat exchange tubes in adjacent rows in said preheat zone are in vertical alignment with each other, and the fins on the heat exchange tubes in said waste heat recovery zone are in vertical alignment with each other.
 31. The retort apparatus as claimed in claim 28, wherein each fin is comprised of an elongated sheet of heat conducting material which surrounds each of said heat exchange tubes in a respective row, and has opposite ends in contact with opposing side walls of said elongated housing.
 32. The retort apparatus as claimed in claim 31, wherein a plurality of said fins are spaced from each other and positioned on said heat exchange tubes of each respective row.
 33. The retort apparatus as claimed in claim 28, further comprising venting means including a plurality of rows of elongated U-shaped bodies connected between opposing walls of said elongated housing defining the cracking and distillation zone and connected in an inverted position so that the open end of each U-shaped body faces downwardly in assembled position, with one row of said elongated U-shaped bodies separating a plurality of rows of said heat exchange tubes in transverse relation to the latter.
 34. The retort apparatus as claimed in claim 1, wherein said housing is defined by a plurality of connected walls, said heat exchange tubes extend out of said housing through opposing ones of said walls, and further including manifold means surrounding said opposing walls for supplying heated gas to said heat exchange tubes.
 35. The retort apparatus as claimed in claim 34, wherein said cracking and distillation zone includes a plurality of vertically arranged sections extending from a lowermost section to an uppermost section, and said manifold means includes input manifold means for supplying said heated gas to said lowermost section, output manifold means for receiving said heated gas from the heat exchange tubes in said uppermost section, and connecting manifold means for fluidly connecting the heat exchange tubes of said plurality of sections.
 36. The retort apparatus as claimed in claim 35, further including recirculation means for recirculating said heated gas from said output manifold means to said input manifold means.
 37. The retort apparatus as claimed in claim 35, further including gas burner means for supplying said heated gas to said input manifold means.
 38. The retort apparatus as claimed in claim 35, further including vent means for venting said heated gas from said output manifold means.
 39. A retort apparatus for recovering hydrocarbons from oil shale comprising:a. an elongated housing, having passage means end to end therethrough, inlet means to permit delivery of crushed shale into one end of the housing for movement along said passage means, and outlet means in communication with the end of the passage means remote from the inlet means for removing the spent oil shale from the passage means, said passage means disposed serially between the inlet means and the outlet means to define in the passage means a drying zone, a preheat zone, a cracking and distillation zone, and a waste heat recovery zone, b. a plurality of heat exchange means connected in said housing for heat exchange with the crushed oil shale moving through said passage means, c. circulating means connecting the respective one of said plurality of heat exchange means in the preheat zone with the respective one of said plurality of heat exchange means in the waste heat recovery zone for passing waste heat from said waste heat recovery zone to said preheat zone, d. said respective one of said heat exchange means in each of said preheat zone and said waste heat recovery zone including a plurality of heat exchange tubes arranged in a plurality of vertical rows, the heat exchange tubes in each row being staggered with respect to heat exchange tubes of adjacent rows, and fins positioned on said heat exchange tubes, said fins on said heat exchange tubes in adjacent rows being in vertical alignment with each other, e. auxiliary heating means connected to the one of said plurality of heat exchange means in said cracking and distillation zone to raise the temperature of the crushed oil shale moving therethrough to the critical temperature for separating hydrocarbon vapors from said crushed oil shale, f. separating means connected in said housing for communication with said cracking and distillation zone to withdraw and condense the hydrocarbon vapors released from the crushed oil shale moving through the passage means and to recover the same, g. means connected to the housing to control movement of crushed oil shale through said passage means, h. means for sensing the pressures in said passage means on opposite sides of said cracking and distillation zone, i. means for adjusting the pressure in said cracking and distillation zone in response to the sensed pressures and to a pressure greater than the pressures in the other zones, and j. means adjacent the outlet means for removing spent oil shale discharged therefrom.
 40. The retort apparatus as claimed in claim 39, wherein each fin is comprised of an elongated sheet of heat conducting material which surrounds each of said heat exchange tubes in a respective row, and has opposite ends in contact with opposing side walls of said elongated housing.
 41. The retort apparatus as claimed in claim 40, wherein a plurality of said fins are spaced from each other and positioned on said heat exchange tubes of each respective row. 